Method of producing an amide utilizing a microorganism

Description

[0001] This invention relates to a method of producing an amide utilizing a microorganism. More particularly, the present invention is concerned with a method of producing an amide in which a nitrile is hydrated by the action of a microorganism belonging to the genus Rhodococcus to obtain the corresponding amide and the amide is isolated. The method is advantageous in productivity and in that a variety of amides can be produced from the corresponding nitriles.

[0002] Acrylamide and methacrylamide are known as the amides which are most important in the industrial field. Acrylamide is utilized as a polymer aggregating agent, a paper reinforcing agent, a fiber improving material or the like. Further, important utilization is being developed in the field of petroleum product recovery. On the other hand, methacrylamide is widely utilized as the ingredient of a coating composition, adhesive, photocrosslinkable composition or the like since it has a well-balanced characteristic with respect to hydrophilicity and hydrophobicity as well as excellent heat resistance and photocrosslinkability.

[0003] Known in the art is a process for producing an amide in which a nitrile is hydrated by using reduced copper as a catalyst. This process is disadvantageous in that regeneration of the catalyst is difficult and that isolation and purification of the amide produced need laborious procedures. Hence, it has been desired to develop a novel process which can be advantageously used in the industrial field.

[0004] In line with this effort for development of a novel and advantageous process, several proposals have recently been made which concern a process using a microorganism. For example, in U.S. Patent No. 4,001,081 (corresponding to British Patent No. 1,535,307 and Japanese Patent Application Laid-Open Specification No. 51-86186/1976), it is proposed to produce an amide by treating a nitrile with a microorganism belonging to a member selected from the group consisting of the genera Bacillus, Bacteridium, Micrococcus and Brevibacterium. In U.S. Patent No. 4,248,968 (corresponding to British Patent No. 2,018,240 and Japanese Patent Application Publication No. 56-17918/1981), it is proposed to produce an amide by treating a nitrile with a microorganism belonging to the genus Corynebacterium or Nocardia. In European Patent Application Laid-open Specification No. 0 093 782 (corresponding to Japanese Patent Application Publication No. 59-37951/1984), it is proposed to produce an amide by treating a nitrile with a microorganism belonging to the genus Pseudomonas. However, all of the above-mentioned microorganisms have not a desirably high activity to convert a nitrile to the corresponding amide. Further, the proposed processes using the above-mentioned microorganisms, in most cases, have a drawback that the amount of organic acids formed as by-products is not on a level that is allowable from the viewpoint of industrial production. Therefore, there is still a strong demand in the art for a novel process for producing an amide which is free from the above-mentioned drawbacks of the prior art.

[0005] The inventors have made extensive and intensive studies to find and isolate a microorganism which has a desirably high activity to specifically convert a nitrile to the corresponding amide. As a result, it has unexpectedly been found that certain microorganisms belonging to the genus Rhodococcus are extremely effective for the purpose. Based on this unexpected finding, the present invention has been completed.

[0006] According to the present invention, there is provided a method of producing an amide which comprises the steps of:

(1) subjecting a nitrile to be hydrated to the action of a microorganism in an aqueous medium, said microorganism being selected from the group consisting of Rhodococcus sp. AK-32 (Fermentation Research Institute Accession No. FERM BP-1046) and Rhodococcus sp. AK-33 (Fermentation Research Institute Accession No. FERM BP-1047) which has been incubated in a culture medium containing a culturing nitrile as a carbon and nitrogen source, to thereby convert the nitrile to be hydrated to the corresponding amide; and

(2) isolating the amide from the aqueous medium,

[0007] In the method of the present invention, a nitrile is subjected to the action of a microorganism belonging to the genus Rhodococcus and having the ability to hydrate the nitrile. The above-mentioned microorganisms are highly active to a wide variety of nitriles as set out hereinbelow even at low temperatures, for example about 10 °C. Due to the high activity of the microorganism at low temperatures, the method of the present invention can be conducted at low temperatures so that the microorganism can be used for a prolonged period of time.

[0008] The microorganism strains Rhodococcus sp. AK-32 and Rhodococcus sp. AK-33 to be employed in the present invention have been deposited with the Fermentation Research Institute of the Agency of Industrial Science and Technology and assigned Accession Nos. FERM BP-1046 and FERM BP-1047, respectively. These microorganism strains have the following bacteriological and chemotaxonomic properties.

[0009] As a result of comparison of the foregoing bacteriological and chemotaxonomic properties to the descriptions in Bergey's Manual of Determinative Bacteriology (eighth edition 1974) and in The Prokaryotes, A Handbook on Habitats, Isolation, and Identification of Bacteria (1981), it is noted that the strains Rhodococcus sp. AK-32 and Rhodococcus sp. AK-33 are aerobic, gram-positive rods having no motility. Further, it is noted that they are in a long bacillary form of rods but not in a hypha form and they grow with branching and fragmentation, and later break and split into a coccoid or short bacillary form of rods. The peptidoglycan of their cell walls has a meso-diaminopimelic acid, and the N-acyl group thereof is of glycolyl type. The GC analysis of their somatic fatty acids shows the predominance of straight-chain fatty acids and the presence of mycolic acid along with the characteristic existence of 10-methyloctadecanic acid. Therefore, it is apparent that these strains belong to the genus Rhodococcus. Differences are observed between these strains in growth conditions and acid formation from saccharide.

[0010] As the suitable nitriles to be subjected to the action of a microorganism, there may be mentioned, for example, saturated aliphatic nitriles such as acetonitrile, propionitrile, succinonitrile and adiponitrile, ethylenically unsaturated nitriles such as acrylonitrile and methacrylonitrile, aromatic nitriles such as benzonitrile and phthalodinitrile and heterocyclic nitriles such as nicotinonitrile.

[0011] The specified microorganism belonging to the genus Rhodococcus and having the ability to hydrate nitriles may be incubated in, for example, a culture medium containing, as a carbon and nitrogen source, a nitrile such as propionitrile, isobutylonitrile, methacrylonitrile or the like. However, the microorganism may preferably be incubated in a culture medium which contains, besides a nitrile as a carbon and nitrogen source, a carbon source such as glucose, aldose or the like, a nitrogen source such as ammonium sulfate, ammonium nitrate or the like and an organic nutrient source such as an yeast extract, malt extract, pepton, meat extract or the like. To this medium, an inorganic nutrient source such as a phosphate, sodium, potassium, iron, magnesium, manganese, zinc or the like may optionally be added. The pH value of the culture medium may be generally in the range of from 5 to 9, preferably in the range of from 6 to 8. The culturing temperature may be generally in the range of from 20 to 35 °C, preferably in the range of from 27 to 32 °C. Under these conditions, the culturing may be carried out aerobically for 2 to 5 days.

[0012] According to the method of the present invention, a nitrile in an aqueous medium is subjected to the action of the specified microorganism belonging to the genus Rhodococcus and having the ability to hydrate the nitrile. In practicing the method of the present invention, various modes are possible. For example, there can be mentioned a mode in which the microorganism is incubated in the presence of a nitrile to be hydrated and another mode in which a nitrile is brought into contact with the culture containing the incubated cells of the microorganism or with the cells of the microorganism harvested from the culture. There can also be mentioned a further mode in which a nitrile is contacted with the cells obtained by disrupting the collected microorganism. Moreover, there is still a further mode in which the cells of the microorganism are fixed onto a carrier and then they are brought into contact with a nitrile. The above-mentioned harvest of cells may be carried out by centrifugation or other known technique, and the disruption of cells may be effected mechanically, e.g. by means of a homogenizer, or by supersonic vibration.

[0013] In the present invention, the culture containing incubated cells as it is may be brought into contact with a nitrile, as mentioned above. Alternatively, the cells harvested from the culture may be dispersed in water or a buffer such as phosphate buffer (for example, pH 7-9), and contacted with a nitrile, thereby causing the nitrile to be hydrated rapidly to form the corresponding amide. In the present invention, the conditions for hydrating nitriles are not critical. In general, the method of the present invention may be practiced as follows. An aqueous suspension containing 0.1 to 5 % by weight of cells of the microorganism and 0.2 to 10 % by weight of a nitrile, which suspension has a pH value of 5 to 10, is prepared, and the suspension is maintained at 0 to 30 °C for a period of about 2 minutes to about 8 hours to hydrate the nitrile. In this connection, it is noted that the nitrile to be used in the present invention generally exhibits a high toxicity to organism. In view of this, it is preferred that the concentration of the nitrile in the reaction medium be controlled within a level, for example 2 % by weight or less, which does not adversely affect the hydration reaction. Therefore, as a preferred method, there may be mentioned a method in which the nitrile is gradually added continuously or intermittently in the course of the hydration reaction so that the deactivation of the microorganism can be prevented. In this connection, it is noted that lowering of the temperature of the reaction medium is also effective to retain the activity of the microorganism for a prolonged period of time.

[0014] From the resulting reaction mixture, the amide produced may be isolated by means of customary techniques such as centrifugation, membrane separation, vacuum concentration, crystalization, etc., thereby to obtain a purified amide. According to need, coloring substances, impurities and the like may be removed, before the vacuum concentration, crystalization or the like, by the treatment using an activated charcoal, an ion exchange resin or the like.

[0015] According to the method of the present invention in which use is made of a microorganism belonging to the genus Rhodococcus and having the ability to hydrate a nitrile, an amide can be produced at a low cost on a commercial scale. Due to the high activity of the above-mentioned microorganism and high selectivity of the hydration reaction of nitriles for the corresponding amides, various amides can be produced with a conversion ratio of almost 100 %, i.e. with an extremely small amount of or without formation of by-products. Further, owing to the high activity of the microorganism even at low temperatures, the hydration of a nitrile can be carried out at low temperatures, so that the microorganism can be used for a prolonged period of time.

[0016] The present invention will now be explained in more detail with reference to the following Examples but they should not be construed as limiting the scope of the present invention.

Example 1

(1) Culture

[0017] Rhodococcus sp. AK-32 was cultured under the following conditions.
1) Culture Medium:

Trypton	1.7 wt%
Soy peptone	0.3 wt%
Glucose	0.25 wt%
Isobutyronitrile	0.5 wt%
NaCℓ	0.5 wt%
K₂HPO₄	0.25 wt%
pH	7.3

2) Cultural Conditions:
30 °C/4 days

(2) Hydration of Methacrylonitrile

[0018] The cells in the cultured broth thus obtained were collected by centrifugation, washed with physiological saline and used for the hydration as follows. 0.2 Part by weight (on a dry basis) of the cells, 2.0 parts by weight of methacrylonitrile and 97.8 parts by weight of 0.05 M phosphate buffer (pH 7.0) were mixed to prepare a reaction mixture. The temperature of the reaction mixture was maintained at 30 °C. Five minutes later, the reaction mixture was analyzed by gas chromatography. As a result, it was found that 2.5 parts by weight of methacrylamide were contained in the reaction mixture, and that the methacrylonitrile remaining unreacted and by-product such as methacrylic acid or the like were not found in the reaction mixture. This shows that the methacrylonitrile was hydrated almost quantitatively to methacrylamide and the reaction was completed.

Comparative Example 1

(1) Culture

[0019] Corynebacterium sp. N-774 (Fermentation Research Institute Accession No. 4446) was incubated under the following conditions.
1) Culture Medium:

Glucose	1.0 wt%
Peptone	0.5 wt%
Yeast extract	0.3 wt%
Malt extract	0.3 wt%
pH	7.2

2) Culture Conditions:
28 °C/3 days

(2) Hydration of methacrylonitrile

[0020] After incubation, the cultured broth was subjected to centrifugation to separate the cells from the cultured broth. The thus obtained cells were washed with water and then dried. 3 Parts of the dried cells were mixed with 97 parts of water. Then, methacrylonitrile was added dropwise to the resulting mixture maintained at 30 °C at a rate of 3 parts per hour under stirring while controlling the pH at 8.5 using potassium hydroxide, to effect hydration reaction. After the reaction for 4 hours, the addition of methacrylonitrile was stopped, but the stirring was continued for further 30 min to complete the reaction. After completion of the reaction, the reaction mixture was centrifuged to remove the cells. Thus, there was obtained a clear solution. The content of methacrylamide in the solution was determined by liquid chromatography and found to be 13.0 wt%, which means that the yield is 95 mole %.

Example 2

(1) Culture

[0021] Rhodococcus sp. AK-32 was cultured under the following conditions.
1) Culture Medium:

Glucose	1.0 wt%
Meat extract	1.0 wt%
Peptone	1.0 wt%
Isobutyronitrile	0.25 wt%
NaCℓ	0.1 wt%
KH₂PO₄	0.1 wt%
MgSO₄·7H₂0	0.05 wt%
FeSO₄·7H₂0	0.005 wt%
MnSO₄·4-5H₂0	0.005 wt%
(NH₄)₂SO₄	0.1 wt%
KNO₃	0.1 wt%
pH	7.0

2) Culturing Conditions:
30 °C/3 days

(2) Hydration of Nitriles

[0022] The cells of the microorganism were collected in substantially the same manner as in Example 1.

[0023] Using various nitriles, the hydration of the nitriles was carried out under the following conditions.

Cell (on a dry basis)	0.2 wt%
Substrate nitrile	2.0 wt%
0.05M phosphate buffer (pH 7.0)	97.8 wt%
Temperature	10 °C
Reaction time	5 minutes

[0024] The results obtained are shown below.

[0025] The above-mentioned amounts were determined by gas chromatography, except for the amounts of amides having a high boiling point as those obtained from succinonitrile, adiponitrile, benzonitrile, terephthalonitrile and nicotinonitrile. The amounts of these amides were determined by liquid chromatography.

Example 3

(1) Culture

[0026] Rhodococcus sp. AK-33 was cultured under substantially the same conditions as in Example 2.

(2) Hydration of Acrylonitrile

[0027] Cells of the microorganism were collected from the cultured broth obtained in substantially the same manner as in Example 1. To 1 ℓ of 0.05 M phosphate buffer (pH 7.0) were added the cells in an amount of 10 g (on a dry basis) to prepare a dormant cell dispersion. At intervals of 20 minutes, acrylonitrile was added to the dispersion in an amount of 20 g at a temperature of 2 to 3 °C. Just before every addition of acrylonitrile, the concentrations of acrylonitrile and acrylamide in the reaction mixture were determined by gas chromatography. From the results, it was found that the amount of the produced acrylamide increased linearly with the lapse of reaction time until 5 hours after the initiation of the hydration reaction, and 450 g/ℓ-buffer of acrylamide was produced. At that time, the hydration reaction was still be able to proceed further but the reaction rate was lowered and, therefore, the reaction was terminated.

[0028] The yield of acrylamide was about 100 mole %, and the quantity of acrylic acid formed as a by-product was only about 0.1 % based on the acrylonitrile added.

Comparative Example 2

(1) Culture

[0029] Pseudomonas chlororaphis B-23 (Fermentation Research Institute Accession No. 187) was cultured under the following conditions.
1) Culture Medium:

Dextrin	0.5 wt%
K₂HPO₄	0.2 wt%
MgSO₄·7H₂0	0.02 wt%
Isobutyronitrile	0.2 wt%
NaCℓ	0.1 wt%
pH	7.0

2) Culturing Conditions:
28 °C/3 days

(2) Hydration of Acrylonitrile

[0030] The cells of the microorganism were separated from the cultured broth and washed with water. The thus obtained cells were dispersed in phosphate buffer (pH 7.0) at a concentration of 20 g (on a dry basis)/ℓ-buffer to prepare a dormant cell dispersion. To the dispersion, acrylonitrile was intermittently added at a temperature of 0 to 4 °C so that the concentration of acrylonitrile was maintained at 0.4 M. The amount of the produced acrylamide increased linearly with the reaction time, and 7.5 hours after the initiation of the reaction, 400 g/ℓ-buffer of acrylamide was produced. The reaction seemed to proceed further but was terminated at this stage since the reaction mixture became viscous.

[0031] The yield of acrylamide was about 99 mole %, and the quantity of acrylic acid formed as a by-product was about 0.7 % based on the acrylonitrile added.

Example 4

(1) Culture

[0032] Rhodococcus sp. AK-32 was cultured in substantially the same manner as in Example 2.

(2) Hydration of Methacrylonitrile

[0033] The cells were collected in substantially the same manner as in Example 3. To 1 ℓ of 0.05M phosphate buffer (pH 7.0) were added 5 g (on a dry basis) of the cells to prepare a dormant cell dispersion. Methacrylonitrile was added to the dispersion at intervals of one hour in an amount of 20 g at a temperature of 2 to 3 °C. Just before every addition of methacrylonitrile, the concentration of methacrylonitrile remaining unreacted in the reaction mixture was determined by gas chromatography. About 5 hours after the initiation of the addition, methacrylamide began to separate out as crystals. Thereafter, the addition of methacrylonitrile was continued at a decreased rate of 20 g per 2 hours because the reaction rate was lowered to cause some methacrylonitrile to be left unreacted. The hydration reaction was continued for 25 hours. As a result, 245 g of methacrylamide crystals were obtained. The reaction mixture was kept refrigerated at 4 °C for 1,600 hours. Then, 20 g of methacrylonitrile was added to the mixture to effect a further hydration reaction at 2 to 3 °C. 2 hours later, no unreacted methacrylonitrile was detected. The yield of methacrylamide was about 100 mole %, and the quantity of methacrylic acid formed as a by-product was as little as about 0.1 % based on the methacrylonitrile added.

Example 5

(1) Culture

[0034] Rhodococcus sp. AK-32 was cultured in substantially the same manner as in Example 2.

(2) Hydration of Methacrylonitrile

[0035] The cells were collected in substantially the same manner as in Example 3. The cells were fixed to calcium alginate gels to obtain immobilized cells. 25 g of the immobilized cells (0.5 g cells, on a dry basis) were added to 75 g of 0.5 weight % aqueous solution of calcium chloride (pH 7.0) to prepare a dispersion of immobilized dormant cells. Methacrylonitrile was added to the dispersion at intervals of one hour in an amount of 2 g at a temperature of 2 to 3 °C. Just before every addition of methacrylonitrile, the concentration of methacrylonitrile remaining unreacted in the reaction mixture was determined by gas chromatography. About 5 hours after the initiation of the addition, methacrylamide began to separate out as crystals. Thereafter, the addition of methacrylonitrile was continued at a decreased rate of 2 g per 2 hours because the reaction rate was lowered to cause some methacrylonitrile to be left unreacted. The hydration reaction was continued for 15 hours. As a result, 10.8 g of methacrylamide crystals were obtained. The quantity of methacrylic acid formed as a by-product was as little as about 0.3 % based on the methacrylonitrile added.

Example 6

[0036] The culture medium described in Example 2 was put into each of two 500 ml conical flasks in an amount of 200 g. In the medium, the strain Rhodococcus sp. AK-33 was incubated under agitation using a rotary shaker at 220 rpm at 30 °C for 24 hours. Then, the incubation in one of the two flasks was stopped to determine the cell concentration. As a result, it was found that the cells were present at a concentration of 1050 ppm. To the other flask was added methacrylonitrile at a rate of 0.25 g per hour and incubation was conducted under the above-mentioned conditions. The incubation was stopped 72 hours after the initiation of the incubation to determine the concentration of the cells and the amount of methacrylamide produced in the flask. The amount of methacrylamide was determined by gas chromatography. It was found that the cell concentration increased to 5100 ppm, and that the methacrylamide produced in the flask was 11.2 g. In the culture medium, no methacrylic acid was detected whereas 500 ppm of methacrylonitrile was found to remain unreacted.

Example 7

[0037] Rhodococcus sp. AK-32 was cultured under substantially the same conditions as in Example 2. Then, 20 g of the cultured broth containing the cells was put into a 50 mℓ conical flask in which a magnetic rotor was placed. The flask was put in a water bath maintained at a temperature of 4 °C. The cultured broth was stirred for 2 hours. Thereafter, methacrylonitrile was added to the cultured broth at a rate of 0.4 g per hour. 8 Hours after the initiation of addition of methacrylonitrile, methacrylamide began to separate out as crystals. The addition of methacrylonitrile was further continued. 18 Hours after the initiation of addition of methacrylonitrile, it became impossible to rotate the magnetic rotor because a large amount of precipitated crystals accumulated in the flask. So the addition of methacrylonitrile was stopped. The resulting slurry in the flask was diluted with water to 1000 g, thereby to dissolve the methacrylamide crystals in the water. The methacrylamide concentration of the solution was determined by gas chromatography to be 0.91 wt%. Neither methacrylonitrile nor methacrylic acid was detected in the reaction mixture.

Example 8

[0038] Rhodococcus sp. AK-32 was cultured in substantially the same manner as in Example 2. The culture broth thus obtained was subjected to centrifugation to collect cells. The collected cells were washed with an aqueous solution of potassium chloride (0.05 M, pH 7.0) and subjected to further centrifugation. To 2 g of the thus obtained dormant cells of strain AK-32 (water content, 80 %) was added 40 g of 0.05 M phosphate buffer (pH 7.0) to prepare a dormant cell dispersion. The dispersion was treated by means of a homogenizer for 30 min while maintaining the temperature at 0 to 5 °C, thereby to disrupt the cells. To 98 parts by weight of the thus treated dispersion containing the disrupted cells was added 2.0 parts by weight of methacrylonitrile to effect the hydration thereof at 30 °C in substantially the same manner as in Example 1. 10 Minutes after the initiation of the hydration reaction, the reaction mixture was analyzed. As a result, the formation of 2.5 wt% based on the reaction mixture (yield: 100 mole %) of methacrylamide was confirmed.

Claims

1. A method of producing an amide which comprises the steps of:

(1) subjecting a nitrile to be hydrated to the action of a microorganism in an aqueous medium, said microorganism being selected from the group consisting of Rhodococcus sp. AK-32 (Fermentation Research Institute Accession No. FERM BP-1046) and Rhodococcus sp. AK-33 (Fermentation Research Institute Accession No. FERM BP-1047) which has been incubated in a culture medium containing a culturing nitrile as a carbon and nitrogen source, to thereby convert the nitrile to hydrated to the corresponding amide; and

(2) isolating the amide from the aqueous medium,

2. A method according to claim 1, wherein said nitrile to be hydrated is a member selected from the group consisting of saturated aliphatic nitriles, ethylenically unsaturated aliphatic nitriles, aromatic nitriles and heterocyclic nitriles.

3. A method according to claim 2, wherein said nitriles to be hydrated is a member selected from the group consisting of acetonitrile, propionitrile, succinonitrile and adiponitrile.

4. A method according to claim 2, wherein said nitrile to be hydrated is acrylonitrile or methacrylonitrile.

5. A method according to claim 2, wherein said nitrile to be hydrated is benzonitrile or phthalodinitrile.

6. A method according to claim 2, wherein said nitrile to be hydrated is nicotinonitrile.

7. The method according to claim 1, wherein said culturing nitrile as a carbon and nitrogen source is a member selected from the group consisting of propionitrile, isobutyronitrile and methacrylonitrile.

Revendications

1. Procédé de préparation d'un amide, qui consiste:

(1) à soumettre un nitrile à hydrater à l'action d'un microorganisme dans un milieu aqueux, ce microorganisme étant choisi parmi le groupe consistant en Rhodococcus sp. AK-32 (Fermentation Research Institute Accession No FERM BP-1046) et Rhodococcus sp. AK-33 (Fermentation Research Institute Accession No FERM BP-1047) qui a été mis à incuber dans un milieu de culture contenant un nitrile de culture comme source de carbone et d'azote, de manière à transformer le nitrile à hydrater en l'amide correspondant ; et

(2) à isoler l'amide du milieu de culture.

2. Procédé suivant la revendication 1, dans lequel le nitrile à hydrater est choisi parmi les nitriles aliphatiques saturés, les nitriles aliphatiques à insaturation éthylénique, les nitriles aromatiques et les nitriles hétérocycliques.

3. Procédé suivant la revendication 2, dans lequel le nitrile à hydrater est choisi parmi l'acétonitrile, le propionitrile, le succinotrile et l'adiponitrile.

4. Procédé suivant la revendication 2, dans lequel le nitrile à hydrater est l'acrylonitrile ou le méthacrylonitrile.

5. Procédé suivant la revendication 2, dans lequel le nitrile à hydrater est le benzonitrile ou le phtalodinitrile.

6. Procédé suivant la revendication 2, dans lequel le nitrile à hydrater est le nicotinonitrile.

7. Procédé suivant la revendication 1, dans lequel le nitrile de culture servant de source de carbone et d'hydrogène est choisi parmi le propionitrile, l'isobutyronitrile et le méthacrylonitrile.

Ansprüche

1. Verfahren zur Herstellung eines Amids, welches die folgenden Stufen umfaßt :

(1) ein zu hydratisierendes Nitril wird in einem wäßrigen Medium der Einwirkung eines Mikroorganismus unterworfen, wobei der Mikroorganismus unter Rhodococcus sp. AK-32 (Hinterlegungsnummer FERM BP-1046 beim Fermentation Research Institute) und Rhodococcus sp. AK-33 (Hinterlegungsnummer FERM BP-1047 beim Fermentation Research Institute) ausgewählt wird, der in einem Kulturmedium, welches ein zur Züchtung dienendes Nitril als Kohlenstoff- und Stickstoffquelle enthält, inkubiert worden ist, wobei das zu hydratisierende Nitril in das entsprechende Amid übergeführt wird und

(2) Isolieren des Amids aus dem wäßrigen Medium.

2. Verfahren gemäß Anspruch 1, bei dem das zu hydatisierende Nitril aus der aus gesättigten aliphatischen Nitrilen, ethylenisch ungesättigten aliphatischen Nitrilen, aromatischen Nitrilen und heterocyclischen Nitrilen bestehenden Gruppe ausgewählt ist.

3. Verfahren gemäß Anspruch 2, bei dem das zu hydratisierende Nitril aus der aus Acetonitril, Propionitril, Bernsteinsäurenitril und Adiponitril bestehenden Gruppe ausgewählt ist.

4. Verfahren gemäß Anspruch 2, bei dem das zu hydratisierende Nitril Acrylnitril oder Methacrylnitril ist.

5. Verfahren gemäß Anspruch 2, bei dem das zu hydratisierende Nitril Benzonitril oder Phthalsäuredinitril ist.

6. Verfahren gemäß Anspruch 2, bei dem das zu hydratisierende Nitril Nicotinsäurenitril ist.

7. Verfahren gemäß Anspruch 1, bei dem das zur Züchtung als Kohlenstoff- und Stickstoffquelle dienende Nitril aus der aus Propionitril, Isobutyronitril und Methacrylnitril bestehenden Gruppe ausgewählt ist.